Tubular digester

ABSTRACT

Contiguous flow anaerobic digester for mechanization of organic matter and production of fertilizer powering the conditions and performance of the anaerobic digestion process, through homogenization of the sludge and process temperature, wherein the digester is tubular shaped and comprises a biogas exhaust valve at the top of the digester. One end of the digester has a sludge outlet connection, a water- and gas-tight zipper that is resistant to the corrosive elements of digestion, and an outlet. The opposite end of the digester has a mud inlet, and a water- and gas-tight zipper that is resistant to the corrosive elements of digestion, wherein said digester further comprises at its base a gas irrigation system for biogas recirculation composed of a polymeric material resilient to the corrosive elements of anaerobic digestion.

The present invention relates to an anaerobic digester that is tubular shaped made from a series of polymers of high mechanical and chemical performance and resistant to UV, abrasion and other climatic conditions within which the anaerobic digestion of the organic material occurs (digestate) producing methane, where the biogas obtained is recirculated into the reactor via modular circuits, gas diffusers, and compounds of polymeric material resistant to corrosion produced by the anaerobic digestion. Such recirculation system of biogas, allows the hydrodynarnic control of the reactor improving the operation and the process.

BACKGROUND OF THE INVENTION

At the industry and experimental level, different types of reactors designed to create optimal conditions for anaerobic digestion of organic waste are identified. At the industry level, according to the EPA (United States Environmental Protection Agency) in 2011 34% of the reactors were plug flow (PF) modified, 30% were full mix (MC), 13% were covered lagoons, the 13% were horizontal FP, and the remaining 10% was divided between reactors “Upflow Anaerobic Sludge Blanket” (UASB) to adehesa biomass and other gaps partially covered. In the past decade, the FP was the most common reactor. Only in recent years have MC digesters increased their presence in the U.S. market. On the other hand, in Europe the most common type of reactor is the MC. This is due to the fact that most of the biogas market in Europe is covered by the German companies that opt for this technology in building agricultural decentralized plants.

In a plug flow reactor, the most important function of the recirculation system of the digestate is to recycle the microorganisms grown during anaerobic digestion to inoculate fresh waste to the influent, i.e., increasing the concentration of the catalyst right where it is most needed. Another function of the recirculation is to increase the agitation of the reactor. By increasing the flow velocity increases turbulence in the reactor with it, the agitation. This implies that the agitation system by biogas and digestate recirculation can have the same purpose: to homogenize the content of the reactor. For example, in an EGSB (“expanded granular sludge bed”) reactor a high flow recirculation, combined with the internal resistance due to the granular sludge is normally applied, it creates a good agitation. Another example is the agitation by pumped of the digestate in a reactor at MC. Note that to get a good stirring of the reactor by stirring, is necessary to move from laminar flow to turbulent flow by increasing the recirculation flow and/or hydraulic barriers.

Various anaerobic digesters are known from the prior art that aim to produce methane From the decomposition of organic material and then produce biogas. At the same time it is observed that there are various designs of reactors used for this purpose, as well as building materials used. It is also known front the prior art that for best results in the process of generation of gas from the anaerobic decomposition it is necessary to agitate the material residing within the reactor to maximize the action of the bacterial organisms and thus have better control of the pH, pressure and temperature of the biodigestion process.

ES 8602551 describes an anaerobic digestion tank for use in sewage wells with gas circulation pipes which open into the bottom of the tank, targeting the gas bubbling through the wells to shake thereto, where some these pipes are associated individually with heat exchange envelopes of heaters. Each gas circulation pipe opens to the lower part of the tank so that the gas exiting from the pipe does so in the direction towards the base of the tank and the bottom of the wells, so that the wells are drawn into below to collide on the tank base to remove sedimented materials and thus avoid the accumulation of these materials in the bottom of the tank.

For its part U.S. Pat. No. 5,185,079 describes an anaerobic process carried out in a pond where biological reaction occurs under anaerobic conditions and the pond is operated in a fill sequence. When waste enters into the reactor pond it is mixed with biogas or liquid recirculating and waste feed continues until the reactor is filled to its maximum predetermined level. Anaerobic reaction occurs with continuous or intermittent mixing and once it discontinues enables biomass to settle forming low solids. Alter sufficient time in the settling cycle, the liquid over low solids on the reactor is discarded decreasing the reactor contents to the predetermined low liquid level. The mixture of gas or liquid is recirculated again and she excess biomass from the reactor periodically wasted.

Document US 20060231488 describes a tubular digester system including a heat holding tank connected to a manifold which feeds one or multiple parallel injection pumps that force the filling through valves and into one or several parallel digesters hulls. The biogas produced by the digester is pressurized due to a liquid column effluent created by a high output. The filling material is put into contact with microorganisms that promote the generation of biogas which is stored by a collector whose release is controlled by a valve or regulator.

Finally, the document US 2002/0079266 discloses a system for converting the cellulose contained in the raw material into useful materials, which contains in one or more sludge feeders, two or more anaerobic pressurized digesters connected in parallel, each reactor containing a stirrer, a or more feed ports, one or more discharge ports, optional pressure regulator, and a reaction chamber, which supports the reaction solution containing anaerobic microorganisms that convert the aqueous slurry at least methane and enriched effluent. This invention is characterized by the use of high pressure for the process which range from more than 10 psi to 265 psi, in order to provide conditions tor the decomposition of cellulose into useful materials.

Therefore, none of the prior art proposes the technical advantage of providing an anaerobic digestion reactor that facilitates the digestion of different types of organic matter on a continuous basis, in an economical, simple, accessible and adaptable to different agro-industrial processes way, being easily scalable through material and structural principles of geotechoical to lower costs and by control systems that made more flexible operability, optimizing their performance by means of hydrodynamic control reactor.

DESCRIPTION OF THE INVENTION

The objective of the present invention is to propose a tubular anaerobic digester for methanization of organic matter and production of substrate for fertilizers or agricultural applications by stirring biogas recirculation, generating a flow boosts the internal hydraulic, allowing a partial homogenization temperature and digestate processing that strength, giving stability, reducing maintenance costs, extending the range of total solids (TS) to be digested between 2% to 15% and allowing congestion.

The proposed solution is a tubular reactor made from a series of polymers with high mechanical properties, chemical which has incorporated a hermetically sealed inspection element that connects the interior with the exterior that allows the operation and maintenance of the system. It also has an instrumentation and automated control of the conditions within the reactor that allows control the process and adapt to different working conditions of anaerobic digestion.

The digester also has a biogas recycle system which allows control of internal hydrodynamic by modular reactor through modular diffusers arranged in circuits size and shape of the reactor to recirculate the gas produced by the methanization reincorporating it into the reactor.

The recirculation system is fixed to the base of the reactor in order to inject tire gas in form of bubbles rising from the bottom of the digester by the mud stirring it and potentiating the action of methanizer bacteria avoiding sedimentation of solids in the bottom of the reactor, allowing to administer such agitation according the convenience of the process.

Thanks to these characteristics, it provides an increase in the rate of mixture of microorganisms tor a better execution of the process and a uniform temperature is obtained by reducing this mismatch problems pH mode.

Further, due to gas recirculation process generated, it is possible to obtain better dissolution of CO2 thus increasing influent original alkalinity allowing the digestion of volatile solids range going from 15% to 20%, also allowing co-occurrence of different substrates.

Advantageously, thanks to the design of the reactor and due to the recirculation process explained above, it is possible to significantly reduce the residence time hydraulic (HRT), Thus it is clear to observe the advantages obtained from the invention proposed and which could not be obtained from the prior art since a design of tubular biodigester to solve the technical problem proposed in the manner proposed in this document is not observed.

The proposed invention will be better understood, and other objects, details, characteristics and advantages thereof will demonstrate more clearly with reference to the accompanying drawings below.

DESCRIPTION OF THE FIGURES

FIG. 1 shows a side view of a tubular anaerobic digester.

FIG. 2 shows a front view of the tabular anaerobic digester.

FIG. 3 shows a roar view of the tubular anaerobic digester.

FIG. 4 shows a plan view of the tubular anaerobic digester where gas diffusers circuits are observed.

DETAILED DESCRIPTION OF THE INVENTION

With reference to FIG. 1, the digester (A) from the present invention having at its top a biogas valve (G) arranged to control the output of the generated gas into the reactor tor distribution is observed. Preferably the valve has been implemented according to the standard for natural gas network distribution.

The gas recirculation system from (H) is disposed in the bottom of the reactor. There is a drain (F) connected to the output of the digester (A) whose purpose is to evacuate fluids from the organic material towards the outside.

FIG. 2 shows a front view of the digester (A) which comprises a control system winch includes a thermometer (B) to measure the temperature at the outlet of the digester (A), it is also provided with a gauge (C) for measuring the pressure inside the reactor.

Under the mud inlet connection (D′) is provided a hermetically sealed inspection element (E) which is sealed to water and gas, as well as resistant to corrosive elements of digestion, whose function is to connect the inside to the outside of the biodigester (A) to allow maintenance work.

As seen in FIG. 3 that has been placed in the bottom of the digester (A) a slurry inlet (D′) used to be connected to the pipes carrying the organic material to be deposited in the digester (A) and a thermometer (B′) to measure the temperature at the inlet of the digester. Furthermore it has been incorporated a hermetically sealed inspection element, which is sealed to water, gas and corrosive elements from the digestion (E′).

FIG. 4 shows the layout of the gas recirculation system in this case separated in two independent diffusers circuits that allow the gas to be recirculated through the interior of the digester (A).

The biodigester is a container made with a series of polymers with high chemical resistance to stress, UV, abrasion and other weather conditions which is made according to the availability of muds, ie, can vary in size depending on the amount of organic material to be treated within him or the gas demand required to be extracted.

The design also makes it possible that additionally to vary its size it can be arranged in series or parallel connected modules being adjustable to different scales treatments.

Experimentally, a tubular digester was designed as explained above 3.4 m in diameter, a length of 18.8 m and capacity of 170 m³. Its materiality is composed of a number of polymeric materials, where each has its functional role.

The materials used allow chemical resistance to alkali, organic acids and volatile compounds as well as UV resistance, abrasion and water. As well as thermal insulation. The inlet and out of muds were made of PVC pipe of 16 cm.

Regarding the recirculation system were used microperforated polymeric hoses 24 m for front circuit and rear.

In the preferred embodiment, the organic material mixed with water is deposited into the digester (A) through a pipe connected to the inlet of sludge (D′). The temperature inside the digester (A) is measured by the thermometer (B). Once deposited organic material begins the process of digestion of organic matter due to the ideal conditions inside the digester achieved in tire present invention.

The gas generated by the digestion process is retained inside the reactor and part of it is recirculated by a gas blower (blower) by means of the front and rear gas recirculation system through micro apertures which have the hoses of the system, allowing tire to flow in the form of bubbles from the bottom of the digester passing through the organic matter and simultaneously generating a hydrodynamic movement.

Biogas valve (G) allows the gas to be removed from digester (A) to be consumed or used in a home network or the network type of convenience.

During the biodigestion process it can be required emptying the digester, for this purpose we have the drain path (F) to empty its contents towards the outside of the digester (A).

Meanwhile, the organic material that has been treated within the digester is removed for subsequent use as substrate for fertilizers or agricultural applications or recirculated to the digester (D′), thus proceeding to introduce a .new quantity of organic material forming the natural inoculation for the process of biogas generation within the tubular anaerobic digester that is claimed below. 

1. Continuous flow anaerobic digester to methanization of organic matter and production of substrate for fertilizers or agricultural applications powering the conditions and the performance of the anaerobic digestion process, by means of hydrodynamic control that partially homogenizes the mass and the energy of the process characterized in that the digester (A) consists of a reactor of a series of polymeric flexible materials with high mechanical and chemical performance, comprising an exhaust valve of biogas (G) located at the top of the digester (A), wherein one end of the digester (A) has a sludge outlet connection (D), a path for drain and a inspection element (E) water-tight and gas-tight, as well as resistant to corrosive elements of digestion, that communicates the interior with the exterior, and where the opposite end of the digester (A) have a mud inlet (D′) and a inspection element (E) water-tight and gas-tight, as well as resistant to corrosive elements of digestion, that communicates the interior with the exterior, wherein said digester (A) further comprises at its base a gas recirculation system (H) for biogas recirculation consisting of modular diffusers circuits arranged according to reactor size and shape, composed of a polymeric material resilient to the corrosion of the elements of anaerobic digestion.
 2. Anaerobic digester according to claim 1, characterized in that one end of the digester (A) further comprising a control system consisting of automated instrumentation such as thermometer, manometer, valves and probes, inter alia.
 3. Anaerobic digester according to claim 1, characterized in that the gas coming from the gas circulation system (H) is recirculated in the form of bubbles of biogas thanks to the micro-perforations of the hoses forming said recirculation system (H).
 4. Anaerobic digester according to claim 3, characterized in that the recirculated gas comes from the same digester (A) or collaborative digesters connected in series or parallel.
 5. (canceled)
 6. Anaerobic digester according to claim 1 characterized in that said biogas valve (G) allows connection to the natural gas network or various units of energy use.
 7. Anaerobic digester according to any of the preceding claims characterized in that the mud inlet (D′), the mud output connection (D), the drain path (F) and the biogas valve (G) are constructed of material with resistance to the corrosion produced by the anaerobic digestion of compounds.
 8. Method for obtaining biogas into an anaerobic digester according to claim 1 enhancing hydrodynamic control of the reactor, allowing an operating range of 2-15% total solids, which prevents sedimentation at the base of the reactor, facilitates installation and maintenance, allows optimum co-digestion of various substrates of the process, characterized in that it comprises the steps of: depositing organic material mixed with water into the digester (A) according to claims 1-6 through a pipe connected to the mud inlet (D′); controlling parameters such as pressure, temperature, pH, hydraulic residence time (HRT), total solids (TS), among others inside the biodigester once deposited the organic material begins the process of digestion of organic matter due to the ideal conditions achieved inside the biodigester of the present invention; retain the gas generated by the digestion process into the reactor and recirculating part of it by means of the gas recirculation system of biogas, which via the micro-perforations which have the hoses of the system, allowing the gas in the form of bubbles to flow from the base of the digester homogenizing in a partial way the matter and energy of the reactor, thereby obtaining the hydrodynamic control required.
 9. The method for obtaining biogas according to claim 8, further comprising the step of allowing the gas to be removed from digester (A) through valve the biogas valve (G) to be consumed or used in a home network or the network type of convenience.
 10. The method for obtaining biogas according to claim 9, characterized in that further comprise the step of evacuating the contents to the outside of the digester (A) through a drain path (F) in case the biodigestion process requires it.
 11. The method for obtaining biogas according to claim 9, characterized in that further comprise the step of removing the organic material that has already been treated within the biodigestor (A) through a connection pipe connected to the mud outlet (D′) for its subsequent use as fertilizer. 